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CHRISGAS: Clean Hydrogen-rich Synthesis Gas
The International Freiberg Conference on IGCC & XtL Technologies
Freiberg 2005-06-16Krister Ståhl M.Sc.
KS Ducente AB
The Issue Addressed
Transport Fuel Usage in EU 15
1998 Gas and diesel 244 Mtoe2010 Gas and diesel (prognosis) 304 Mtoe
1998 Biofuel 0,5 Mtoe2000 Biofuel 0,7 Mtoe2010 Biofuel (target 5,75%*) 17,5 Mtoe2020 Biofuel (target 8-10%, under revision)
*Directive on Biofuels for Transport, 2003/30/EC
National Policy
Swedish National Energy Agency aim:to attain a 10% market share for biofuel in 2012
Interagency* Strategy Paper: Gasification to synthesis gas is a key technology to use the biomass available to produce large quantities of renewable transport fuels
* STEM, EPA, Road Transport Authority
First Generation BiofuelsCosts and Energy Efficiency
• Sugar cane ethanol 30 €/MWh50%
• Grain or sugar ethanol 30-50 €/MWh30-50%
• RME 60 €/MWh30%
Second Generation BiofuelsCosts and Energy Efficiency
• Cellulosic ethanol 70-80 €/MWh20-35 %
• Methanol/DME 40-60 €/MWh50-60%
• FT fuel < 70 €/MWh40-50%
• Hydrogen (target 36€/MWh) ? (gas, liquid)
Sydkraft IGCC Plant, Värnamo
• Op. 1993-2000
• Air blown gasifier, 18 bar for GT
• Typhoon GT
• 18 MW thermal,
• 4 ton/hr feed
• 8 500 hours op.
• 3 600 hours GT
•1998-2002– Swedish Energy Agency, Environmental Protection
Agency and Road Traffic Authority:Joint Renewable Fuel Policy emphasis on Biomass-based Synthesis Gas RD&D
– Studies of use of the Värnamo Plant after IGCC demonstration program in 1998 and 2000-2001 indicating technical feasibility for synthesis gas generation objective
Project Development
EC FP6 call 2003.ML
Relevant subjects in the 2003.ML CfP
–R&D of cost efficient biofuel production systems from ligno-cellulosic biomass
– R&D & optimisation of energy-efficient, cost-effective technologies for producing of hydrogen-rich gas from biomass
CHRISGAS Summary
• System studies related to the large-scale use of and
its impact on the environment and society at large
and Training activities are included in this IP
•The hub of the Integrated Project (IP) is the existing, unique 18 MW biomass-fuelled pressurised air-blown gasification combined cycle CHP plant at Värnamo
• The Värnamo plant will be refurbished to
oxygen gasification to produce a hydrogen-rich gas.
• This IP offers already in 2007 gasification RD&D
at large scale at a lower cost than alternatives
CHRISGASClean Hydrogen-rich Synthesis Gas
Synthesis Gas
Natural Gas
Gasification
Reforming
Fischer-Tropsch
Methanol
Biomass and waste
H2
DME
CHRISGAS Objectives
To demonstrate the production ofa clean hydrogen-rich synthesis gas
(within a 5 year period at 18 MWth,3 500 Nm3/hr H2 equivalent)
based on:– steam/oxygen-blown gasification of biomass
– hot gas cleaning (to remove particulates)
– steam reforming (of tar and light hydrocarbons,
incl. CH4)
Växjö Värnamo Biomass Gasification Center, VVBGC
• Non-profit making project-based company
• Large-scale test platform
• European biomass gasification centre
Key Data of CHRISGAS• 16 Partners
– 9 IND of which 7 SME– 4 HE– 3 RES – 2 OTHER
• 7 member states: S, DK, D, ES, NL, FI, I• 5 years duration
• Budget 15.6 M€ + costs outside project• 9.5 M€ EU grant
• Partner ind. 4.6 M€• 1.5 M€ STEM grant +7 M€ grant outside
CHRISGAS Partners
Sweden: Växjö University (co-ordinator), Växjö VärnamoBiomass Gasification Centre (VVBGC), AGA-Linde, Catator, KS Ducente, Royal Institute of Technology (KTH), S.E.P. Scandinavian Energy Project, TPS Termiska Processer, VäxjöEnergiDenmark: TK EnergiFinland: ValutecGermany: FZ Jülich, Linde, Pall SchumacherItaly: University of BolognaNetherlands: Technical University DelftSpain: CIEMAT
The VVBGC Plant, Värnamo
•Steam/oxygen blown gasification
•Hot gas filtration of raw gasification gas
•Reforming of tars and methane
•Water gas shift to hydrogen-rich gas
•Planning for further downstream rebuilds
Parallel R&D activities– Feedstock biomass logistics
– Biomass drying integration
– Pressurised fuel feeding (piston feeder)
– Gasification, hot synthesis gas characterisation (laboratory and bench-scale work)
– High temperature filtration/cleaning
– Catalytic steam reforming (decay & deactivation)
– Shift gas catalyst characterisation
Other activities
– Training (university courses and ”hands-on”)– Dissemination– Process studies (e.g. novel methods of
contaminants removal)– System studies (e.g. H2, methanol, DME, F-T)– Socio-economic impact
- emissions- jobs created- regional growth
CHRISGAS Status•2003
–March: Application for FP6 IP project
– May-August: Positive evaluation by the EC– September- into 2004: Preparation of
•Technical Annex and Consortial Agreement
•2004– January: STEM co-financing decision – up to September: Preparation of
•Technical Annex and Consortial Agreement•Co-financing arrangements
– August 2004:Purchase of plant and plant IPR – October: Kick-off meeting– December: Contract signed
CHRISGAS Plans• 2005
– Conceptual engineering of plant– Balance of financing– Other project activities
• 2006-2007– Plant rebuild– Other project activities
• 2007-2009 – Plant operation– Other project activities
– Other projects outside CHRISGAS– FP7 Technical Platform on Advanced Biomass Conversion?
Follow-up activities(Phase II, from end 2007)
PHASE II Automotive fuels
Stakeholder driven
plans to install a complete GTL facility
DME, methanol, FT, hydrogen etc.
CHRISGAS
Hot Gas
Cleaning
CHRISGAS offers
• From the VBGC plant– Establish raw syngas production in 2007 – Syngas and potential GTL products for fleet tests
after 2007 – VVBGC as platform for
• a training center• customer RTD work on i.e. gas cleaning, liquid fuels,
FC:s, H2
CHRISGAS offers
• To Europe and Sweden in relation to 2003/30/EC
– A show-case project of Swedish and European ambitions to accelerate the implementation of the Directive
– Create a center of excellence on an European scale for training and technical know-how in the area of gasification for liquid biofuels